Temperature control system for a heat transfer fluid in a circulation loop, temperature control method

Abstract

A control system (1) for the temperature of a heat transfer fluid (F) configured to transfer heat to a fluid to be heated (Q) from a cryogenic reservoir (R), the control system (1) comprising: a circulation loop (2) of the heat transfer fluid (F) comprising a motor branch (21) and a reservoir branch (22); a first motor exchanger (41), configured to heat the heat transfer fluid (F) to a second temperature (T2) above a maximum operating temperature (Tmax); a mechanical pump (3) configured to circulate the heat transfer fluid (F) in the circulation loop (2), so as to transfer a first part of the heat transfer fluid (F) to the fluid to be heated (Q) in a second motor exchanger (42) and to cool the heat transfer fluid (F) to a third temperature (T3) below the maximum operating temperature (Tmax), before its exit from the motor enclosure (EN-M).Figure from the summary: Figure 2.

Description

Title of the invention: System for controlling the temperature of a heat transfer fluid in a circulation loop, temperature control method Technical field

[0001] The present invention relates to the field of aircraft comprising a fluid stored in a cryogenic tank, for example fuel supplying a turbomachine.

[0002] It is known to store a fluid, for example fuel such as hydrogen, in liquid form to limit the size and mass of the aircraft tanks. For example, the fuel is stored at a temperature of the order of -253 to -251°C (20 to 22 Kelvins) in a cryogenic tank of the aircraft.

[0003] In this example, in order to be injected into the combustion chamber of a turbomachine, the fuel must be conditioned, i.e. pressurized and heated, in order to allow optimal combustion. Conditioning is for example necessary to reduce the risk of icing / solidification of the water vapor contained in the air circulating in the turbomachine, in particular, at the fuel injectors of the turbomachine.

[0004] With reference to [Fig. 1], there is shown a conditioning system SC AA comprising a fuel circuit CQ connected at the inlet to a cryogenic tank R and at the outlet to the combustion chamber of a turbomachine M. The conditioning system SCAA comprises a mechanical pump P for driving a flow of fuel Qc from upstream to downstream in the fuel circuit CQ. In a known manner, the aircraft comprises an engine enclosure EN-M (for example a nacelle) and a tank enclosure EN-R, separate and remote from the engine enclosure EN-M. The cryogenic tank R is mounted in the tank enclosure EN-R and the turbomachine M is mounted in the engine enclosure EN-M.

[0005] The SCAA conditioning system also comprises a temperature control system 101 of a heat transfer fluid F which provides calories to the fuel flow Qc in order to heat it so that it can be injected into the turbomachine M with an optimal temperature and pressure.

[0006] In the prior art, for example, patent application FR2005628A1 discloses a temperature control system 101, also shown in [Fig. 1], which comprises a circulation loop 102 for the heat transfer fluid F and a mechanical recirculation pump 103 for driving the heat transfer fluid F in motion in the circulation loop 102. In the control system 101 described in document FR2005628A1, the heat transfer fluid F extracts calories from hot sources Cm available on board the aircraft (for example the heat from the lubricating oil of the turbomachine M, the calories at the turbine outlet, heat from the nozzle), via an engine heat exchanger 104 mounted on the circulation loop 102 in the assembly enclosure EN-M. The temperature control system 101 also comprises a tank heat exchanger 105 for heating the fuel flow Qc of the SCAA conditioning system from the calories transferred by the heat transfer fluid F.

[0007] In practice, the heat sources Cm present in the engine enclosure EN-M make it possible to heat the heat transfer fluid F via the engine exchanger 104 from a first temperature T1 to a second temperature T2. The heat transfer fluid F then circulates at the temperature T2 in the circulation loop 102 to the tank exchanger 105 to heat the fuel flow Qc at the outlet of the mechanical pump P, therefore in the tank enclosure EN-R. In an embodiment not shown, the architecture described in patent FR2005628A1 also comprises a heat exchanger mounted in the tank enclosure EN-R to heat the heat transfer fluid F once again by means of the heat sources present in the tank enclosure EN-R, such as the air at the cabin outlet or the thermal discharges from the electrical / electronic components on board for example.

[0008] However, in a known manner, in such a control system 101, the temperature of the heat transfer fluid F must not exceed a predetermined temperature range. In practice, the temperature T2 of the heat transfer fluid F at the outlet of the engine enclosure EN-M must be lower than a maximum operating temperature Tmax, in order to be able to convey the heat transfer fluid F as close as possible to the tank R without risking damage to the structure of the aircraft through which the circulation loop 102 passes, such as the wings of the aircraft for example. On the other hand, the temperature T1 of the heat transfer fluid F at the inlet of the engine enclosure EN-M must be higher than a minimum operating temperature Tmin, in order to avoid any risk of icing of the heat sources Cm in the engine exchanger 104. In other words, the control of the temperature in the circulation loop 102 is highly constrained.

[0009] To limit the maximum temperature of the heat transfer fluid F at the outlet of the engine exchanger 104, it is known to increase the circulation flow rate of the heat transfer fluid F in the circulation loop 102, which has many drawbacks. Indeed, the mass and the size of the piping of the circulation loop 102 are very significant, which is not desirable in an aircraft. In addition, the aerothermal performances of the heat exchangers are limited, which increases the distribution defects in the heat exchangers. The mechanical pump is also forced to operate at a higher flow rate, which increases its electrical consumption.

[0010] The invention thus aims to eliminate at least some of these drawbacks by proposing a new system for controlling the temperature of the heat transfer fluid in the circulation loop allowing heating which is efficient and reliable, without limiting the temperature range of the heat transfer fluid. PRESENTATION OF THE INVENTION

[0011] The invention relates to a system for controlling the temperature of a heat transfer fluid configured to transfer calories to a fluid to be heated, the fluid to be heated coming from a cryogenic tank in which it is stored at an initial temperature and configured to be conveyed to an engine via a fluid circuit, the cryogenic tank being mounted in a tank enclosure, the engine being mounted in an engine enclosure separate from the tank enclosure, the tank enclosure being configured to operate at a temperature below a maximum operating temperature, the engine enclosure being configured to operate at a temperature above a minimum operating temperature, the control system comprising: • a heat transfer fluid circulation loop extending both in the tank enclosure and in the engine enclosure, the circulation loop comprising: • a motor branch extending in the motor enclosure between a motor inlet point and a motor outlet point, the heat transfer fluid circulating from upstream to downstream between the motor inlet point and the motor outlet point, the heat transfer fluid having a first temperature at the motor inlet point, the first temperature being higher than the minimum operating temperature of the motor enclosure, • a tank branch extending into the tank enclosure between a tank inlet point and a tank outlet point, the heat transfer fluid circulating from upstream to downstream between the tank inlet point and the tank outlet point, the engine outlet point being fluidically connected to the tank inlet point, the tank outlet point being fluidically connected to the engine inlet point, • at least one first engine exchanger, mounted on the engine branch, configured to heat the heat transfer fluid to a second temperature higher than the first temperature, from calories transferred by at least one hot fluid available in the engine enclosure, the second temperature being higher than the maximum operating temperature of the tank enclosure, • at least one first tank exchanger, mounted on the tank branch, configured to heat the fluid to be heated from the heat transfer fluid to a primary temperature, • at least one second engine exchanger, mounted on the engine branch, configured to heat the fluid to be heated from the heat transfer fluid to a secondary temperature, higher than the primary temperature, • at least one mechanical pump configured to circulate the heat transfer fluid in the circulation loop, so as to: • in the second engine exchanger, transfer a first portion of calories from the heat transfer fluid to the fluid to be heated and cool the heat transfer fluid to a third temperature lower than the second temperature, the third temperature being lower than the maximum operating temperature, so as to heat the heat transfer fluid in the first engine exchanger to a temperature higher than the maximum operating temperature and to lower this temperature in the second engine exchanger below the maximum operating temperature, before it leaves the engine enclosure and enters the tank enclosure, • in the first tank exchanger, transfer a second portion of calories from the heat transfer fluid to the fluid to be heated and cool the heat transfer fluid to a fourth temperature, lower than the third temperature, so as to heat the fluid to be heated to the secondary temperature, so as to preheat the fluid to be heated before it leaves the tank enclosure.

[0012] The control system according to the invention allows the heat transfer fluid to be heated by the first engine exchanger to a temperature higher than the maximum operating temperature, which makes it possible not to increase the circulation flow rate of the heat transfer fluid in the circulation loop. A limited flow rate advantageously makes it possible to limit the mass and size of the piping in the circulation loop, since the latter does not need to be reinforced to withstand particularly high flow rates. A limited flow rate also makes it possible to optimize the aerothermal performance of the heat exchangers mounted on the circulation loop, which makes it possible to limit the risks of faulty distribution of the fluids in the heat exchangers. In addition, the mechanical pump is not forced to operate at a particularly high flow rate, which makes it possible to limit its wear and its electrical consumption.

[0013] The control system according to the invention also allows heating of the fluid to be heated in two stages. In a first stage, the fluid to be heated is heated in the first tank exchanger up to the primary temperature allowing to ensure the best compromise between simplicity and safety of implementation of the circuit. In a second step, the fluid to be heated is heated in the second engine exchanger to the secondary temperature sufficiently high to allow, for example, the injection of fuel into the turbomachine to supply it.

[0014] In one embodiment, the control system comprises at least one second tank exchanger, mounted on the tank branch, the second tank exchanger being configured to heat the heat transfer fluid from calories transferred by at least one hot fluid available in the tank enclosure. In a first embodiment, the second tank exchanger is configured to be mounted downstream of the first tank exchanger, the second tank exchanger then being configured to heat the heat transfer fluid from the fourth temperature to the first temperature. The heat transfer fluid can thus be cooled more significantly in the first tank exchanger by transferring more calories to the fuel flow. This makes it possible to further lower the heat transfer fluid flow rate. In a second embodiment, the second tank exchanger is configured to be mounted upstream of the first tank exchanger.Such a second tank exchanger makes it possible to use the heat available on board the aircraft and thus limit, for example, the size and bulk of an exchanger in a turbomachine.

[0015] In this embodiment, the fourth temperature of the heat transfer fluid at the outlet of the first tank exchanger is between -123°C (150K) and 2°C (275K), making it possible to lower the temperature of the heat transfer fluid in the first tank exchanger locally lower than the minimum operating temperature in order to then heat it. This makes it possible to further lower the flow rate of heat transfer fluid.

[0016] In a second embodiment, the fourth temperature of the heat transfer fluid at the outlet of the first reservoir exchanger is between 2°C (275K) and 77°C (350K). The temperature of the heat transfer fluid is thus greater than 2°C (275K) when entering the heat exchanger with a heat source, making it possible to limit any risk of icing of the hot sources in the heat exchanger.

[0017] Preferably, the second temperature of the heat transfer fluid at the outlet of the first engine exchanger is between 227°C (500K) and 377°C (650K), which makes it possible to reduce the circulation flow rate of the heat transfer fluid, thus allowing the use of lighter and less bulky piping. The heat transfer fluid can thus be heated to a temperature higher than the maximum operating temperature, i.e. 227°C (500K), since it will start by transferring calories to the fuel flow in the engine enclosure.

[0018] In a preferred embodiment, the third temperature of the heat transfer fluid at the outlet of the second engine exchanger is between 77°C (350K) and 227°C (500K). The temperature of the heat transfer fluid is thus lower than the maximum operating temperature when leaving the engine enclosure. This allows the heat transfer fluid to circulate between the engine enclosure and the tank enclosure, for example in the structure of an aircraft (for example in the wings) without this presenting any risk of damage. In addition, the transport of the fluid does not need to be carried out in special pipes to withstand high temperatures, pipes which would have significant mass, size and / or cost.

[0019] In one embodiment, the third temperature of the heat transfer fluid at the outlet of the second engine exchanger is less than 202°C (475K), preferably less than 177°C (450K). Such a temperature allows the use of aluminum pipes, instead of stainless steel pipes as is the case in the prior art, allowing a significant weight saving.

[0020] In one embodiment, the control system comprises a controllable valve mounted on the circulation loop between the second engine exchanger and the first tank exchanger, so as to direct a first portion of the heat transfer fluid to the first tank exchanger and to the engine enclosure and a second portion of the heat transfer fluid to the first engine exchanger, so as to allow a lower flow rate of the heat transfer fluid to the engine enclosure. Such a controllable valve makes it possible to regulate the circuit while maintaining optimal extraction of calories in the engine sources.

[0021] In one embodiment, the control system comprises a regenerative heat exchanger, mounted on the engine branch, the regenerative heat exchanger being configured to heat the heat transfer fluid upstream of the first engine exchanger by the heat transfer fluid downstream of the first engine exchanger. Thanks to such a regenerative heat exchanger, the heat transfer fluid can be cooled at the outlet of the first reservoir exchanger to a temperature below the minimum operating temperature without this presenting a risk of icing the heat sources in the first engine exchanger. Greater cooling in the first reservoir exchanger allows the heat transfer fluid to transfer more calories to the fluid to be heated (at the same heat transfer fluid flow rate), making it possible to heat the latter more significantly while limiting the electrical consumption of the system.

[0022] The invention also relates to a fuel conditioning system configured to supply an aircraft turbomachine with fuel from a cryogenic tank, the conditioning system extending into the tank enclosure and into the engine enclosure, the cryogenic tank being mounted in the tank enclosure and the turbomachine being mounted in the engine enclosure, the system

[0023]

[0024]

[0025]

[0026]

[0027]

[0028] packaging including: • a fuel circuit connected at the inlet to the cryogenic tank and at the outlet to the turbomachine, a flow of fuel circulating from upstream to downstream in the fuel circuit, • at least one mechanical pump configured to circulate the flow of fuel from the cryogenic tank from upstream to downstream in the fuel circuit, and • a temperature control system as described above. In a preferred embodiment, the primary temperature of the fuel flow at the outlet of the first tank exchanger is between -173°C (100K) and -73°C (200K), which makes it possible to ensure that the fuel is in a gaseous state at the outlet of the first tank exchanger, making it possible to limit the use of specific pipes which would have particular thermal insulation and would therefore be heavier and more cumbersome. Preferably, the secondary temperature of the fuel flow leaving the second engine exchanger is between -73°C (200K) and 27°C (300K), corresponding to the fuel injection temperature in the combustion chamber of the turbomachine, which makes it possible to limit the risk of icing of the injectors mounted in the combustion chamber. The invention also relates to an aircraft comprising a cryogenic tank, a turbomachine and a conditioning system as described above. Finally, the invention relates to a method for controlling the temperature of the heat transfer fluid by means of the control system as described previously, the method comprising the steps of: • heat the heat transfer fluid in the engine enclosure in the first engine exchanger, up to a second temperature higher than the maximum operating temperature of the tank enclosure, • cool the heat transfer fluid in the engine enclosure in the second engine exchanger, to a third temperature lower than the maximum operating temperature, • convey the heat transfer fluid to the tank enclosure. PRESENTATION OF FIGURES The invention will be better understood upon reading the following description, given by way of example, and referring to the following figures, given by way of non-limiting examples, in which identical references are given to similar objects. [Fig.l] is a schematic representation of a conditioning system comprising a control system according to the prior art.

[0029] [Fig.2] is a schematic representation of a packaging system comprising a control system according to one embodiment of the invention.

[0030] [Fig. 3] is a schematic representation of a control system according to a second embodiment of the invention.

[0031] [Fig.4] is a schematic representation of a control system according to a third embodiment of the invention.

[0032] [Fig.5] is a schematic representation of a control system according to a third embodiment of the invention.

[0033] It should be noted that the figures set out the invention in detail to implement the invention, said figures can of course be used to better define the invention where appropriate. DETAILED DESCRIPTION OF THE INVENTION

[0034] With reference to [Fig.2], a conditioning system SC for a fluid to be heated Q from a cryogenic tank R is shown. In this example, the fluid to be heated Q is stored in the cryogenic tank R at an initial temperature Ti of the order of -253°C (20K) to -251°C (22K). At this temperature, the fluid to be heated Q is liquid.

[0035] In this example, the fluid to be heated Q is fuel configured to power an engine, in particular in this example an aircraft turbomachine M. It goes without saying that the fluid to be heated Q could be different, in particular the oxidizer (oxygen) or the inert service gases (nitrogen, CO2). In this example, the turbomachine M is configured to provide propulsion for the aircraft, in particular, by driving at least one propulsion member. Finally, in this example, the fuel is liquid hydrogen, but it goes without saying that the invention applies to other types of fuel, for example, liquid methane or liquefied natural gas.

[0036] As shown in [Fig.2], the cryogenic tank R is mounted in a tank enclosure EN-R and the engine M is mounted in a motor enclosure EN-M, separate from the tank enclosure EN-R. The conditioning system SC extends both in the motor enclosure EN-M and in the tank enclosure EN-R.

[0037] In this example, the conditioning system SC comprises a fuel circuit CQ connected at the inlet to the cryogenic tank R and at the outlet to the turbomachine M, and a mechanical pump P configured to circulate a flow of fuel Qc to be heated from the cryogenic tank R from upstream to downstream in the fuel circuit CQ. It goes without saying that the conditioning system SC could comprise a different number of mechanical pumps P, in particular a number greater than one mechanical pump P.

[0038] The conditioning system SC also comprises a system 1 for controlling the temperature of a heat transfer fluid F according to the invention, configured to transfer calories to the fuel flow Qc so as to heat it so that it can supply the turbomachine M.

[0039] According to the invention, still with reference to [Fig. 2], the control system 1 comprises a circulation loop 2 of the heat transfer fluid F extending both in the tank enclosure EN-R and in the engine enclosure EN-M. The tank enclosure EN-R is configured to operate at a temperature above a minimum operating temperature Tmin to avoid icing the hot sources in the heat exchangers, as will be described in more detail later. By the expression "configured to operate at a temperature", it is meant that the fluids (fuel flow Qc, heat transfer fluid F, hot fluids, etc.) circulate at a temperature above the minimum operating temperature Tmin.Similarly, the EN-M engine enclosure is configured to operate at a temperature lower than a maximum operating temperature Tmax at the outlet of the EN-M engine enclosure, to avoid any risk of damage to the structure of the aircraft during the circulation of the heat transfer fluid F between the EN-M engine enclosure and the EN-R tank enclosure.

[0040] In this example, the minimum operating temperature Tmin is of the order of 2°C (275K). Similarly, in this example, the maximum operating temperature Tmax is of the order of 227°C (500K).

[0041] According to the invention, the circulation loop 2 comprises a motor branch 21, extending in the motor enclosure EN-M between a motor inlet point Pim and a motor outlet point P2m, and a reservoir branch 22, extending in the reservoir enclosure EN-R between a reservoir inlet point Plr and a reservoir outlet point P2r. The motor outlet point P2m is fluidically connected to the reservoir inlet point Plr and the reservoir outlet point P2r is fluidically connected to the motor inlet point Pim, so as to allow the continuous circulation of the heat transfer fluid F in the circulation loop 2.

[0042] The heat transfer fluid F circulates in the engine branch 21 from upstream to downstream between the engine inlet point Pim and the engine outlet point P2m, and in the reservoir branch 22 from upstream to downstream between the reservoir inlet point Plr and the reservoir outlet point P2r.

[0043] The heat transfer fluid F has at the engine inlet point Pim, a first temperature Tl higher than the minimum operating temperature Tmin. In this example, the first temperature Tl is between 2°C (275K) and 90°C (363K). Preferably the first temperature Tl is higher than 2°C (275K).

[0044] Still with reference to [Fig.2], the control system 1 comprises a pump mechanical pump 3 configured to circulate the heat transfer fluid F in the circulation loop 2. It goes without saying that the circulation loop 2 could comprise a different number of mechanical pumps 3. Preferably, the mechanical pump 3 is positioned in the circulation loop 2 so as to receive the heat transfer fluid F having the minimum temperature, so as to take advantage of the maximum density of the heat transfer fluid F, which makes it possible to pump the same mass flow rate at a lower energy cost. In this example, the mechanical pump 3 is mounted in the motor enclosure EN-M, as shown in [Fig.2]. It goes without saying that the mechanical pump 3 could just as easily be mounted in the tank enclosure EN-R, as shown in [Fig.3].

[0045] According to the invention, the control system 1 comprises a first engine exchanger 41, a second engine exchanger 42 and a first tank exchanger 51, mounted on the circulation loop 2.

[0046] The first engine exchanger 41 is mounted in the engine enclosure EN-M on the engine branch 21. The first engine exchanger 41 is of the heat transfer fluid / hot fluid type and is configured to heat the heat transfer fluid F from calories transferred by one or more hot fluid(s) Cm available in the engine enclosure EN-M, for example the heat from the lubricating oil of the turbomachine M, the calories at the turbine outlet, the heat from the nozzle, etc.

[0047] The first engine exchanger 41 is configured to heat the heat transfer fluid F to a second temperature T2 higher than the first temperature TL. More precisely, according to the invention, the second temperature T2 is higher than the maximum operating temperature Tmax, in this example of the order of 227°C (500K). In particular, in this example, the second temperature T2 of the heat transfer fluid F at the outlet of the first engine exchanger 41 is between 227°C (500K) and 377°C (650K), which advantageously makes it possible to limit the circulation flow rate of the heat transfer fluid F in the circulation loop 2.

[0048] The first tank exchanger 51 is mounted in the tank enclosure EN-R on the tank branch 22. The first tank exchanger 51 is of the heat transfer fluid / fluid to be heated Q type, in this example fuel flow Qc, and is configured to heat the fuel flow Qc from the heat transfer fluid F to a primary temperature Tp higher than the initial temperature Ti. Preferably, the primary temperature Tp of the fuel flow Qc at the outlet of the first tank exchanger 51 is between -173°C (100K) and -73°C (200K), so as to ensure that the fuel flow Qc is in a gaseous state at the outlet of the first tank exchanger 51.

[0049] The second engine exchanger 42 is mounted in the engine enclosure EN-M on the engine branch 21. The second engine exchanger 42 is of the heat transfer fluid type / fluid to be heated Q (here fuel flow Qc) and is configured to heat the fuel flow Qc from the heat transfer fluid F to a secondary temperature Ts, higher than the primary temperature Tp. Preferably, the secondary temperature Ts of the fuel flow Qc at the outlet of the second engine exchanger 42 is between -73°C (200K) and 27°C (300K). Such a temperature makes it possible, for example, to limit any risk of icing of the water vapor contained in the air in contact with the fuel injectors in the combustion chamber of the turbomachine M.

[0050] According to the invention, as shown in [Fig. 2], after having been heated by the first engine exchanger 41, the heat transfer fluid F is configured to circulate in the circulation loop 2 successively in the second engine exchanger 42 and in the first tank exchanger 51. In other words, the heat transfer fluid F circulates in the circulation loop 2 between the second engine exchanger 42 and the first tank exchanger 51 in a circulation direction opposite to the circulation direction of the fuel flow Qc in the fuel circuit CQ.

[0051] In the second engine exchanger 42, the heat transfer fluid F is configured to transfer a first portion of calories to the fuel flow Qc. The heat transfer fluid F is then configured to be cooled to a third temperature T3 lower than the second temperature T2. The third temperature T3 is lower than the maximum operating temperature Tmax. The second engine exchanger 42 is thus configured to lower the temperature of the heat transfer fluid F (by heating the fuel flow Qc to the secondary temperature Ts), so that the temperature of the heat transfer fluid F is lower than the maximum operating temperature Tmax at the outlet of the engine enclosure EN-M, allowing its circulation towards the tank enclosure EN-R, for example by passing through the wings of the aircraft.In this example, the third temperature T3 of the heat transfer fluid F at the outlet of the second engine exchanger 42 is between 77°C (350K) and 227°C (500K). In one embodiment, the third temperature T3 of the heat transfer fluid F is less than 202°C (475K), preferably even less than 177°C (450K), which allows the use of aluminum pipes, allowing a control system 1 that is much lighter than known control systems in which the pipes are made of stainless steel.

[0052] In the first tank exchanger 51, the heat transfer fluid F is configured to transfer a second portion of calories to the fuel flow Qc. The heat transfer fluid F is then configured to be cooled to a fourth temperature T4, lower than the third temperature T3, so as to heat the fuel flow Qc to the primary temperature Tp, that is to say so as to preheat the fuel flow Qc before it leaves the tank enclosure EN-R. In this example, the fourth temperature T4 of the heat transfer fluid F at the outlet of the first exchanger tank 51 is between 2°C (275K) and 77°C (350K), preventing any risk of icing of a hot source in circulation loop 2.

[0053] In summary, in the control system 1, the heat transfer fluid F is configured to be cooled in two stages, a first time in the second engine exchanger 42 by transferring a first portion of calories and a second time in the first tank exchanger 51 by transferring a second portion of calories. In other words, in the conditioning system SC, the fuel flow Qc is configured to be heated in two stages, a first time in the first tank exchanger 51 by the second portion of calories present in the heat transfer fluid F and a second time in the second engine exchanger 42 by the first portion of calories present in the heat transfer fluid F.

[0054] In one embodiment, with reference to [Fig. 3], the control system 1 comprises a second tank exchanger 52 mounted in the tank enclosure EN-R on the tank branch 22. The second tank exchanger 52 is configured to heat the heat transfer fluid F from calories transferred by one or more hot fluid(s) Cr available in the tank enclosure EN-R. In a first embodiment, the second tank exchanger 52 is mounted downstream of the first tank exchanger 51, the second tank exchanger 52 is then configured to heat the heat transfer fluid F from the fourth temperature T4 to the first temperature T1.In a second embodiment (not shown), the second tank exchanger 52 is mounted upstream of the first tank exchanger 51 to increase the temperature of the heat transfer fluid F before it enters the first tank exchanger 51, so that the heat transfer fluid F transfers more calories to the fuel flow Qc in the first tank exchanger 51 and heats it to a higher temperature.

[0055] In this embodiment, the fourth temperature T4 of the heat transfer fluid F at the outlet of the first reservoir exchanger 51 is between -123°C (150K) and 2°C (275K).

[0056] In this embodiment, the fourth temperature T4 corresponds to the lowest temperature that the heat transfer fluid F reaches in the entire circulation loop 2. Also, in this example, the mechanical pump 3 is preferably mounted between the first tank exchanger 51 and the second tank exchanger 52, so as to take advantage of the minimum temperature and therefore the maximum density of the heat transfer fluid F, as described previously.

[0057] This document presents an example in which the control system 1 comprises two engine exchangers 41, 42 and one or two tank exchangers 51, 52, it goes without saying that the control system 1 could comprise a different number of engine exchangers 41, 42 and / or tank exchangers 51, 52, in particular a number greater than two tank exchangers and / or a number greater than or equal to two engine exchangers.

[0058] In one embodiment, with reference to [Fig. 4], the control system 1 comprises a controllable valve 6 mounted on the circulation loop 2 between the second engine exchanger 42 and the first reservoir exchanger 51. The controllable valve 6 makes it possible to direct a first portion of the heat transfer fluid F1 towards the first reservoir exchanger 51 and towards the engine enclosure EN-M and a second portion of the heat transfer fluid F2 towards the first engine exchanger 41. A lower flow rate of heat transfer fluid F is thus conveyed towards the engine enclosure EN-M, which makes it possible to regulate the circulation loop 2 while maintaining optimal extraction of calories in the engine sources.

[0059] In this example, the controllable valve 6 is mounted in the engine enclosure EN-M, as shown in [Fig.4]. It goes without saying that the controllable valve 6 could just as easily be mounted in the tank enclosure EN-R.

[0060] In one embodiment, with reference to [Fig. 5], the control system 1 comprises a regenerative heat exchanger Exr, mounted on the circulation loop 2 in the engine enclosure EN-M, i.e. on the engine branch 21. The regenerative heat exchanger Exr is of the heat transfer fluid / heat transfer fluid type and is configured to heat the heat transfer fluid F upstream of the first engine exchanger 41 by the heat transfer fluid F downstream of this first engine exchanger 4L. In other words, the heat transfer fluid F is configured to be preheated upstream of the first engine exchanger 41 by the heat transfer fluid F which will have been heated by the first engine exchanger 4L.

[0061] The heat transfer fluid F is thus configured to enter the engine enclosure EN-M at a temperature T Ibis lower than the minimum operating temperature Tmin and to be reheated in the regenerative exchanger Exr to a temperature higher than the minimum operating temperature Tmin, up to the first temperature Tl, before entering the first engine exchanger 41 to avoid any risk of icing of the heat source. In other words, in the tank enclosure EN-R at the outlet of the first tank exchanger 51, the heat transfer fluid F is configured to be cooled below the minimum operating temperature Tmin, making it possible to transfer more calories to the fuel flow Qc.In this embodiment, the heat transfer fluid F is configured to be preheated from the temperature T Ibis to the first temperature Tl in the regenerative exchanger Exr, then to be heated to a temperature T2bis in the first engine exchanger 4L. The heat transfer fluid F is then configured to be cooled in the regenerative exchanger Exr (by heating the heat transfer fluid F circulating upstream of the first engine exchanger 41) to the second temperature T2 before entering the second exchanger. engine 42.

[0062] In a first embodiment (shown in [Fig.5]), the regenerative heat exchanger Exr is configured to be mounted on the circulation loop 2 upstream of the second engine exchanger 42. In a second embodiment (not shown), the regenerative heat exchanger Exr is configured to be mounted on the circulation loop 2 downstream of the second engine exchanger 42.

[0063] A method for controlling the temperature of the heat transfer fluid F will now be described, with reference to [Fig. 2]. The heat transfer fluid F is at the engine inlet point Pim of the engine enclosure EN-M at a first temperature Tl greater than the minimum operating temperature Tmin. In this example, the first temperature Tl is greater than 2°C (275K).

[0064] The method comprises a first step E1 of heating the heat transfer fluid F in the first engine exchanger 41 of the engine enclosure EN-M, up to a second temperature T2, higher than the maximum operating temperature Tmax. In this example the heat transfer fluid F is heated, in step E1, up to a temperature between 227°C (500K) and 377°C (650K).

[0065] The heat transfer fluid F then circulates in the circulation loop 2 in the engine enclosure EN-M, that is to say in the engine branch 21, up to the second engine exchanger 42. The heat transfer fluid F then passes, in a second step E2, through the second engine exchanger 42 in which it transfers a first part of its calories to the fuel flow Qc. The heat transfer fluid F is thus cooled a first time to the third temperature T3, lower than the maximum operating temperature Tmax. In this example, the heat transfer fluid F is cooled in the second engine exchanger 42 to a temperature between 77°C (350K) and 227°C (500K).

[0066] The heat transfer fluid F is then conveyed, in a step E3, to the tank enclosure EN-R. In a fourth step E4, the heat transfer fluid F passes through the first tank exchanger 51 in the tank enclosure EN-R in which it transfers a second part of its calories to the fuel flow Qc. The heat transfer fluid F is thus cooled a second time to the fourth temperature T4. In this example, the heat transfer fluid F is cooled in the first tank exchanger 51 to a temperature between -123°C (150K) and 2°C (250K).

[0067] The heat transfer fluid F circulates in the circulation loop 2 in the reservoir enclosure EN-R, that is to say in the reservoir branch 22 to be conveyed to the engine enclosure EN-M where it will be reheated in the first engine exchanger 4L

Claims

Claims

1. Fuel conditioning system (SC) configured to supply an aircraft turbomachine (M) with fuel from a cryogenic tank (R) in which it is stored at an initial temperature (Ti), the conditioning system (SC) extending in a tank enclosure (EN-R) and in an engine enclosure (EN-M) separate from the tank enclosure (EN-R), the cryogenic tank (R) being mounted in the tank enclosure (EN-R) and the turbomachine (M) being mounted in the engine enclosure (EN-M), the tank enclosure (EN-R) being configured to operate at a temperature below a maximum operating temperature (Tmax), the engine enclosure (EN-M) being configured to operate at a temperature above a minimum operating temperature (Tmin), the conditioning system (SC) comprising: a fuel circuit (CQ) connected at the inlet to the cryogenic tank (R) and at the outlet to the turbomachine (M), a fuel flow (Qc) circulating from upstream to downstream in the fuel circuit (CQ), at least one mechanical pump (P) configured to circulate the fuel flow (Qc) from the cryogenic tank (R) from upstream to downstream in the fuel circuit (CQ), and a control system (1) for the temperature of a heat transfer fluid (F) configured to transfer calories to the fuel flow (Qc), the control system (1) comprising: a circulation loop (2) of the heat transfer fluid (F) extending both in the tank enclosure (EN-R) and in the engine enclosure (EN-M), the circulation loop (2) comprising: • a motor branch (21) extending in the motor enclosure (EN-M) between a motor inlet point (Pim) and a motor outlet point (P2m), the heat transfer fluid (F) circulating from upstream to downstream between the motor inlet point (Pim) and the motor outlet point (P2m), the heat transfer fluid (F) having a first temperature (Tl) at the motor inlet point (Pim), the first temperature (Tl) being higher than the tem minimum operating temperature (Tmin) of the motor enclosure (EN-M), • a tank branch (22) extending into the tank enclosure (EN-R) between a tank inlet point (Plr) and a tank outlet point (P2r), the heat transfer fluid (F) circulating from upstream to downstream between the tank inlet point (Plr) and the tank outlet point (P2r), the engine outlet point (P2m) being fluidically connected to the tank inlet point (Plr), the tank outlet point (P2r) being fluidically connected to the engine inlet point (Pim), at least one first engine exchanger (41), mounted on the engine branch (21), configured to heat the heat transfer fluid (F) to a second temperature (T2) higher than the first temperature (Tl), from calories transferred by at least one hot fluid (Cm) available in the engine enclosure (EN-M), the second temperature (T2) being higher than the maximum operating temperature (Tmax) of the tank enclosure (EN-R), at least one first tank exchanger (51), mounted on the tank branch (22), configured to heat the fuel flow (Qc) from the heat transfer fluid (F) to a primary temperature (Tp), at least one second engine exchanger (42), mounted on the engine branch (21), configured to heat the fuel flow (Qc) from the heat transfer fluid (F) to a secondary temperature (Ts), higher than the primary temperature (Tp), at least one mechanical pump (3) configured to circulate the heat transfer fluid (F) in the circulation loop (2), so as to: • in the second engine exchanger (42), transfer a first portion of calories from the heat transfer fluid (F) to the fuel flow (Qc) and cool the heat transfer fluid (F) to a third temperature (T3) lower than the second temperature (T2), the third temperature (T3) being lower than the maximum operating temperature (Tmax), so as to heat the heat transfer fluid (F) in the first engine exchanger (41) to a temperature higher than the maximum operating temperature (Tmax) and to lower this temperature in the second engine exchanger (42) below the maximum operating temperature (Tmax), before it leaves the engine enclosure (EN-M) and enters the tank enclosure (EN-R), in the first tank exchanger (51), transfer a second portion of calories from the heat transfer fluid (F) to the fuel flow (Qc) and cool the heat transfer fluid (F) to a fourth temperature (T4), lower than the third temperature (T3), so as to heat the fuel flow (Qc) to the secondary temperature (Ts), so as to preheat the fuel flow (Qc) before it leaves the tank enclosure (EN-R).

2. Conditioning system (SC) according to claim 1, in which the control system (1) comprises at least one second reservoir exchanger (52), mounted on the reservoir branch (22), the second reservoir exchanger (52) being configured to heat the heat transfer fluid (F) from calories transferred by at least one hot fluid (Cr) available in the reservoir enclosure (EN-R).

3. Conditioning system (SC) according to claim 2, in which the fourth temperature (T4) of the heat transfer fluid (F) at the outlet of the first reservoir exchanger (51) is between -123°C (150K) and 2°C (275K).

4. Conditioning system (SC) according to claim 1, in which the fourth temperature (T4) of the heat transfer fluid (F) at the outlet of the first reservoir exchanger (51) is between 2°C (275K) and 77°C (350K).

5. Conditioning system (SC) according to one of claims 1 to 4, in which the second temperature (T2) of the heat transfer fluid (F) at the outlet of the first engine exchanger (41) is between 227°C (500K) and 377°C (650K).

6. Conditioning system (SC) according to one of claims 1 to 5, in which the third temperature (T3) of the heat transfer fluid (F) at the outlet of the second engine exchanger (42) is between 77°C (350K) and 227°C (500K).

7. Conditioning system (SC) according to claim 6, in which the third temperature (T3) of the heat transfer fluid (F) at the outlet of the second engine exchanger (42) is less than 202°C (475K), preferably less than 177°C (450K).

8. Conditioning system (SC) according to one of claims 1 to 7, in which the control system (1) comprises a controllable valve (6) mounted on the circulation loop (2) between the second engine exchanger (42) and the first tank exchanger (51), so as to direct a first part of the heat transfer fluid (F1) towards the first tank exchanger (51) and towards the engine enclosure (EN-M) and a second part of the heat transfer fluid (F2) towards the first engine exchanger (41), so as to allow a lower flow rate of the heat transfer fluid (F) towards the engine enclosure (EN-M).

9. Conditioning system (SC) according to one of claims 1 to 8, wherein the control system (1) comprises a regenerative heat exchanger (Exr), mounted on the engine branch (21), the regenerative heat exchanger (Exr) being configured to heat the heat transfer fluid (F) upstream of the first engine exchanger (41) by the heat transfer fluid (F) downstream of the first engine exchanger (41).

10. Conditioning system (SC) according to one of claims 1 to 9, in which the primary temperature (Tp) of the fuel flow (Qc) at the outlet of the first tank exchanger (51) is between -173°C (100K) and -73°C (200K).

11. Conditioning system (SC) according to one of claims 1 to 10, in which the secondary temperature (Ts) of the fuel flow (Qc) at the outlet of the second engine exchanger (42) is between -73°C (200K) and 27°C (300K).

12. Aircraft comprising a cryogenic tank (R), a turbomachine (M) and a conditioning system (SC) according to one of claims 1 to 11.

13. Method for controlling the temperature of the heat transfer fluid (F) by means of the control system (1) of a conditioning system (SC) according to one of claims 1 to 11, the method comprising the steps of: • heat the heat transfer fluid (F) in the engine enclosure (EN-M) in the first engine exchanger (41), up to a second temperature (T2) higher than the maximum operating temperature (Tmax) of the tank enclosure (EN-R), • cool the heat transfer fluid (F) in the engine enclosure (EN-M) in the second engine exchanger (42), to a third temperature (T3) lower than the maximum operating temperature (Tmax), • convey the heat transfer fluid (F) to the tank enclosure (EN-R).

Images